JP2001113138A - Production method of immersion type membrane cartridge - Google Patents

Production method of immersion type membrane cartridge

Info

Publication number
JP2001113138A
JP2001113138A JP29172799A JP29172799A JP2001113138A JP 2001113138 A JP2001113138 A JP 2001113138A JP 29172799 A JP29172799 A JP 29172799A JP 29172799 A JP29172799 A JP 29172799A JP 2001113138 A JP2001113138 A JP 2001113138A
Authority
JP
Japan
Prior art keywords
membrane
filter plate
filter
cartridge
membrane cartridge
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP29172799A
Other languages
Japanese (ja)
Inventor
Yutaka Yamada
山田  豊
Seiji Izumi
清司 和泉
Tatsuya Uejima
達也 上島
Masaaki Nagano
昌章 永野
Yasunobu Okajima
康信 岡島
Yukio Fujiwara
幸男 藤原
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kubota Corp
Original Assignee
Kubota Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kubota Corp filed Critical Kubota Corp
Priority to JP29172799A priority Critical patent/JP2001113138A/en
Publication of JP2001113138A publication Critical patent/JP2001113138A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)
  • Activated Sludge Processes (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a production method of an immersion type membrane cartridge enhanced durability to aeration. SOLUTION: A resin-made filter plate 22A is cooled at a specified temperature and a filter membrane 22B is arranged to cover the surface of the filter plate 22A in a state contracted by cooling, and the filter membrane 22B is stuck or welded to the filter plate 22A at a water stopping part S formed on the whole periphery along the peripheral part of the filter plate 22A to fix, and the filter membrane 22B is applied a tensile force by elongating the filter plate 22A under a temperature to be used and is stretched.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、浸漬型膜カートリ
ッジの製造方法に関し、し尿処理や合併処理浄化槽等に
おいて使用する固液分離装置に搭載する膜カートリッジ
の製造技術に係るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing a submerged membrane cartridge, and more particularly to a technique for manufacturing a membrane cartridge mounted on a solid-liquid separation device used in a human waste treatment or a combined treatment septic tank.

【0002】[0002]

【従来の技術】従来の固液分離装置としては、例えば図
5〜図7に示すような浸漬型膜分離装置がある。図5〜
図7において、膜分離装置21は、複数枚の平板状膜カ
ートリッジ22と、その下方より膜面洗浄気体を噴出す
る散気装置23とをケース24の内部に配置したもので
ある。ケース24は膜ケース25と散気ケース26とに
分割形成し、散気装置23より噴出する膜面洗浄気体の
全量が膜ケース25内に入り込むように形成している。
2. Description of the Related Art As a conventional solid-liquid separation apparatus, for example, there is an immersion type membrane separation apparatus as shown in FIGS. Figure 5
In FIG. 7, a membrane separation device 21 has a plurality of flat membrane cartridges 22 and an air diffuser 23 for ejecting a membrane cleaning gas from below the cartridges 22 arranged inside a case 24. The case 24 is formed so as to be divided into a membrane case 25 and a diffuser case 26 so that the entire amount of the membrane surface cleaning gas ejected from the diffuser 23 enters the membrane case 25.

【0003】膜カートリッジ22は、ABS樹脂製のろ
板22Aの両表面にろ過膜22Bを配置し、ろ過膜22
Bをその周縁部の止水部Sにおいてろ板22Aに超音波
溶着もしくは接着剤で貼り付けたものである。ろ板22
Aとろ過膜22Bとの間、およびろ板22Aの内部には
透過液流路を形成し、透過液流路に連通する透過液取出
口22Cをろ板22Aの上端縁に形成している。
The membrane cartridge 22 has a filtration membrane 22B disposed on both surfaces of a filter plate 22A made of ABS resin.
B is attached to the filter plate 22A by ultrasonic welding or an adhesive at a water stop portion S on the periphery thereof. Filter plate 22
A permeate flow path is formed between A and the filtration membrane 22B and inside the filter plate 22A, and a permeate outlet 22C communicating with the permeate flow path is formed at the upper end edge of the filter plate 22A.

【0004】各膜カートリッジ22は、透過液取出口2
2Cに接続したチューブ27を介して集水管28に連通
しており、膜透過液を導出する透過液導出管29を集水
管28に接続している。
Each membrane cartridge 22 is provided with a permeate outlet 2
The tube 27 is connected to a water collecting pipe 28 via a tube 27 connected to the 2C, and a permeated liquid outlet pipe 29 for extracting a membrane permeated liquid is connected to the water collecting pipe 28.

【0005】[0005]

【発明が解決しようとする課題】上記した構成におい
て、膜分離装置21を活性汚泥処理施設において使用す
る場合には、曝気槽内部の活性汚泥混合液中に膜分離装
置21を浸漬し、散気装置23より曝気空気を噴出させ
る状態において、原水中の有機物や窒素を活性汚泥によ
り処理している。
In the above configuration, when the membrane separation device 21 is used in an activated sludge treatment facility, the membrane separation device 21 is immersed in an activated sludge mixed liquid in an aeration tank to diffuse air. In a state in which aeration air is jetted from the device 23, organic matter and nitrogen in the raw water are treated with activated sludge.

【0006】活性汚泥混合液は、槽内での水頭を駆動圧
として膜カートリッジ22により重力ろ過し(透過液導
出管29に吸引ポンプを介装することで吸引ろ過も可能
である)、膜カートリッジ22の膜面を透過した透過液
を処理水として透過液導出管29を通じて槽外へ導出す
る。このとき、散気装置23より噴出する曝気空気の気
泡およびそれにより生起される上昇流が、相互に隣接す
る膜カートリッジ22の間の狭い流路(5〜10mmの
幅)を流れることによって、膜カートリッジ22の膜面
を洗浄し、分離機能の低下を抑制して膜分離装置21が
機能不全に至ることを防止している。
[0006] The activated sludge mixture is gravity filtered by the membrane cartridge 22 using the head in the tank as the driving pressure (the suction filtration is also possible by interposing a suction pump in the permeate outlet pipe 29). The permeated liquid permeating through the membrane surface of No. 22 is led out of the tank through a permeated liquid outlet pipe 29 as treated water. At this time, the bubbles of the aerated air ejected from the air diffuser 23 and the upward flow generated by the bubbles flow through the narrow flow path (width of 5 to 10 mm) between the mutually adjacent membrane cartridges 22 to form a membrane. The membrane surface of the cartridge 22 is cleaned to prevent the separation function from deteriorating, thereby preventing the membrane separation device 21 from malfunctioning.

【0007】このように、膜分離装置21の使用時にお
いて、膜カートリッジ22は曝気空気による上昇流に曝
されるので、ろ過膜22Bが上昇流によって上方へ煽ら
れる。この上昇流が気泡に由来する乱流であるために、
図7に示すように、ろ過膜22Bは波打ちながら上部の
止水部Sに押し寄せ、その溶着強度が劣化して止水部S
で疲労破壊が起こり易くなり、このことが膜カートリッ
ジの寿命を左右することになる。
As described above, when the membrane separation device 21 is used, the membrane cartridge 22 is exposed to the upward flow by the aerated air, so that the filtration membrane 22B is moved upward by the upward flow. Because this upward flow is a turbulent flow derived from bubbles,
As shown in FIG. 7, the filtration membrane 22B rushes toward the upper water stop S while waving, and the welding strength of the filter membrane 22B deteriorates, and the water stop S
, Fatigue fracture easily occurs, which affects the life of the membrane cartridge.

【0008】本発明は上記した課題を解決するものであ
り、曝気に対する耐久性を高めることができる浸漬型膜
カートリッジの製造方法を提供することを目的とする。
An object of the present invention is to solve the above-mentioned problems, and an object of the present invention is to provide a method of manufacturing a submerged membrane cartridge capable of improving durability against aeration.

【0009】[0009]

【課題を解決するための手段】上記課題を解決するため
に、請求項1に係る本発明の浸漬型膜カートリッジの製
造方法は、樹脂製のろ板を所定冷却温度下で冷却し、冷
却により収縮した状態のろ板に表面を覆ってろ過膜を配
置し、ろ板の周縁部に沿った全周にわたって形成する止
水部においてろ過膜をろ板に接着もしくは溶着して固定
し、ろ板が使用温度下において伸長することによりろ過
膜に引張力を付与して緊張させるものである。
According to a first aspect of the present invention, there is provided a method for manufacturing a submerged membrane cartridge, comprising: cooling a resin filter plate at a predetermined cooling temperature; A filter membrane is placed over the surface of the filter plate in a contracted state, and the filter membrane is fixed to the filter plate by bonding or welding to the filter plate at a water stop portion formed over the entire periphery along the periphery of the filter plate. Are provided at the operating temperature to give a tensile force to the filtration membrane to thereby tension the filtration membrane.

【0010】請求項2に係る本発明の浸漬型膜カートリ
ッジの製造方法は、樹脂製のろ板に表面を覆ってろ過膜
を緊張状態に配置し、ろ板の周縁部に沿った全周にわた
って形成する止水部においてろ過膜をろ板に接着もしく
は溶着して固定し、ろ過膜を緊張状態に保持するもので
ある。請求項3に係る本発明の浸漬型膜カートリッジの
製造方法は、樹脂製のろ板を所定冷却温度下で冷却し、
冷却により収縮した状態のろ板に表面を覆ってろ過膜を
緊張状態に配置し、ろ板の周縁部に沿った全周にわたっ
て形成する止水部においてろ過膜をろ板に接着もしくは
溶着して固定し、ろ板が使用温度下において伸長するこ
とによりろ過膜に引張力を付与して緊張させるものであ
る。
According to a second aspect of the present invention, there is provided a method of manufacturing a submerged membrane cartridge according to the present invention, wherein a filtration membrane is placed in tension on a resin filter plate so as to cover the surface thereof, and is provided over the entire periphery along the periphery of the filter plate. In the formed water stop portion, the filtration membrane is fixed to the filter plate by bonding or welding to fix the filtration membrane in a tensioned state. In the method for manufacturing a submerged membrane cartridge according to the present invention according to claim 3, the resin filter plate is cooled at a predetermined cooling temperature,
The filter membrane is placed in a tensioned state covering the surface of the filter plate in a state contracted by cooling, and the filter membrane is adhered or welded to the filter plate in a water stop portion formed over the entire periphery along the periphery of the filter plate. The filter is fixed, and the filter plate is stretched at the operating temperature to apply a tensile force to the filtration membrane to thereby tension the filtration membrane.

【0011】[0011]

【発明の実施の形態】以下、本発明の実施の形態を図面
に基づいて説明する。本実施の形態における浸漬型膜カ
ートリッジは浸漬型膜分離装置に使用するものであり、
浸漬型膜分離装置および膜カートリッジの基本的な構造
は、先に図5〜図7において説明したものと同様である
ので、同様の部材には同一番号を付して説明を省略す
る。
Embodiments of the present invention will be described below with reference to the drawings. The immersion type membrane cartridge in the present embodiment is used for an immersion type membrane separation device,
Since the basic structures of the immersion type membrane separation device and the membrane cartridge are the same as those described above with reference to FIGS. 5 to 7, the same members are denoted by the same reference numerals and description thereof is omitted.

【0012】以下に、本実施の形態における膜カートリ
ッジ22の製造方法を図1〜図2を参照して説明する。
ろ板22Aは、線膨張係数が0.08〜0.095mm
/m・℃のABS樹脂からなり、横490mm×縦10
00mm×厚さ6mmの形状を有しており、温度1℃の
上昇で長手方向に約0.1mm伸びる。このろ板22A
を例えば5℃以下の所定冷却温度下で冷却し、冷却によ
り収縮した状態とする。ろ板22Aの両表面に有機膜か
らなるろ過膜22Bを配置し、ろ過膜22Bをその周縁
部の止水部Sにおいてろ板22Aに超音波溶着もしくは
接着剤で固定する。
A method of manufacturing the membrane cartridge 22 according to the present embodiment will be described below with reference to FIGS.
The filter plate 22A has a linear expansion coefficient of 0.08 to 0.095 mm.
/ M ・ ℃ ABS resin, width 490mm × length 10
It has a shape of 00 mm x thickness of 6 mm, and extends about 0.1 mm in the longitudinal direction when the temperature rises by 1 ° C. This filter plate 22A
Is cooled at a predetermined cooling temperature of, for example, 5 ° C. or lower, and is in a state of contraction by cooling. A filtration membrane 22B made of an organic film is arranged on both surfaces of the filter plate 22A, and the filtration membrane 22B is fixed to the filter plate 22A by ultrasonic welding or an adhesive at a water stop portion S on the periphery thereof.

【0013】膜カートリッジ22は、例えば活性汚泥槽
では15℃以上の水温下で使用するので、ろ板22Aは
使用時の温度と冷却時の温度との温度差に応じて伸長
し、長手方向に約1mm以上伸びる。このろ板22Aの
伸長によってろ過膜22Bに引張力が作用し、ろ過膜2
2Bが緊張状態となる。膜カートリッジ22の製造方法
としては、他に図3〜図4に示すものがある。この方法
では、樹脂製のろ板22Aに表面を覆ってろ過膜22B
を配置し、ろ過膜22Bに引張力を付与して緊張状態に
保持する。ろ過膜はポリエステルの不織布(厚さ0.1
〜0.15mm)の両面に有機性の膜剤をコーティング
したものであり、引っ張りにより10%の伸び率を有す
るが、伸ばし過ぎると膜の孔径までが変形し、ろ過性能
に影響を与える恐れがある。このため、ろ過膜22Bは
2〜5%程度引き伸ばした緊張状態に保持する。次に、
ろ板22Aの周縁部に沿った全周にわたって形成する止
水部Sにおいて、ろ過膜22Bをろ板22Aに接着剤も
しくは超音波溶着して固定し、ろ過膜22Bを緊張状態
に保持する。
Since the membrane cartridge 22 is used at a water temperature of 15 ° C. or more in, for example, an activated sludge tank, the filter plate 22A extends according to the temperature difference between the temperature at the time of use and the temperature at the time of cooling. It extends about 1 mm or more. Due to the extension of the filter plate 22A, a tensile force acts on the filtration membrane 22B, and the filtration membrane 2B
2B becomes nervous. As another method for manufacturing the membrane cartridge 22, there is a method shown in FIGS. In this method, the filter membrane 22B is covered with a resin filter plate 22A to cover the surface.
Is arranged, and a tensile force is applied to the filtration membrane 22B to keep it in a tensioned state. The filtration membrane is a polyester nonwoven fabric (thickness 0.1
(0.15 mm) coated with an organic film agent on both sides, and has an elongation of 10% due to stretching. However, if the film is stretched too much, the pore size of the film may be deformed, which may affect the filtration performance. is there. For this reason, the filtration membrane 22B is maintained in a tensioned state extended by about 2 to 5%. next,
In the water stopping portion S formed over the entire periphery along the periphery of the filter plate 22A, the filter membrane 22B is fixed to the filter plate 22A by an adhesive or ultrasonic welding, and the filter membrane 22B is held in a tensioned state.

【0014】また、膜カートリッジ22の製造方法とし
ては、先に説明したものを組み合わせるものがある。こ
の方法では、樹脂製のろ板22Aを5℃以下の所定冷却
温度下で冷却する。この冷却により収縮した状態のろ板
22Aに表面を覆ってろ過膜を配置し、ろ過膜22Bに
引張力を付与して緊張状態に保持する。この状態で、ろ
板22Aの周縁部に沿った全周にわたって形成する止水
部Sにおいて、ろ過膜22Bをろ板22Aに接着もしく
は溶着して固定する。
As a method of manufacturing the membrane cartridge 22, there is a method of combining the above-described methods. In this method, the filter plate 22A made of resin is cooled at a predetermined cooling temperature of 5 ° C. or less. A filtration membrane is arranged so as to cover the surface of the filter plate 22A contracted by the cooling, and a tension is applied to the filtration membrane 22B to maintain the tension state. In this state, the filter membrane 22B is fixed to the filter plate 22A by bonding or welding at the water stopping portion S formed over the entire periphery along the peripheral edge of the filter plate 22A.

【0015】この構成により、ろ過膜22Bには初期の
緊張力に加えてろ板22Aの伸長による引張力が作用
し、ろ過膜22Bが緊張状態に保持される。以上のよう
にして製造した膜カートリッジ22を、活性汚泥処理施
設における膜分離装置21に装着して使用する。この使
用において、散気装置23より噴出する曝気空気の気泡
およびそれにより生起される上昇流は、相互に隣接する
膜カートリッジ22の間の狭い流路(5〜10mmの
幅)を流れることによって、膜カートリッジ22の膜面
を洗浄し、分離機能の低下を抑制して膜分離装置21が
機能不全に至ることを防止する。
With this configuration, in addition to the initial tension, the filtration membrane 22B receives a tensile force due to the extension of the filter plate 22A, and the filtration membrane 22B is maintained in a tensioned state. The membrane cartridge 22 manufactured as described above is used by being mounted on the membrane separation device 21 in the activated sludge treatment facility. In this use, the bubbles of the aerated air ejected from the air diffuser 23 and the upward flow generated by the bubbles flow through the narrow flow path (5 to 10 mm width) between the adjacent membrane cartridges 22. The membrane surface of the membrane cartridge 22 is cleaned to prevent a decrease in the separation function, thereby preventing the membrane separation device 21 from malfunctioning.

【0016】このとき、膜カートリッジ22のろ過膜2
2Bは上昇流によって上方へ付勢力を受けるが、ろ過膜
22Bは緊張状態にあるので、煽られて波打ちながら上
部の止水部Sに押し寄せることがなく、乱流の上昇流に
曝されても常に平坦な膜面を維持する。このため、従来
のように、止水部Sで疲労破壊が起こることがなく、膜
カートリッジ22の寿命を延ばすことができる。また、
ろ過膜22Bが常に平坦な膜面を維持することで、上昇
流が膜面の全体に均一に掃流として作用し、洗浄効果が
高まる。
At this time, the filtration membrane 2 of the membrane cartridge 22
2B receives an urging force upward due to the upward flow, but since the filtration membrane 22B is in a tension state, the filter film 22B is not pushed to the upper water stopping portion S while waving and waving, and is exposed to the turbulent upward flow. Always maintain a flat film surface. For this reason, unlike the related art, fatigue breakage does not occur in the water stopping portion S, and the life of the membrane cartridge 22 can be extended. Also,
Since the filtration membrane 22B always maintains a flat membrane surface, the upward flow uniformly acts as a scavenging flow on the entire membrane surface, and the cleaning effect is enhanced.

【0017】膜カートリッジ22は一定期間にわたって
使用すると浸漬洗浄する。この浸漬洗浄は、膜カートリ
ッジ22に次亜塩素酸ソーダや蓚酸溶液を透過液側から
逆方向に注入し、ろ過膜22Bを薬液に浸漬して洗浄す
る。このため、必要に応じて止水部Sの内側においてろ
過膜22Bをろ板22Aにスポット溶着する。このこと
により、ろ過膜22Bが薬液の注入によって膨らむこと
を防止し、ろ過膜22Bの伸びを小さくし、上昇流およ
び気泡によるろ過膜22Bの煽りを抑制し、膜カートリ
ッジ22の寿命を延ばすことができる。
When the membrane cartridge 22 is used for a certain period, it is immersed and washed. In this immersion cleaning, sodium hypochlorite or oxalic acid solution is injected into the membrane cartridge 22 in the reverse direction from the permeate side, and the filtration membrane 22B is immersed in a chemical solution for cleaning. For this reason, the filter membrane 22B is spot-welded to the filter plate 22A inside the water stop portion S as necessary. Thus, it is possible to prevent the filtration membrane 22B from expanding due to the injection of the chemical solution, reduce the elongation of the filtration membrane 22B, suppress the upward movement of the filtration membrane 22B due to the upward flow and bubbles, and extend the life of the membrane cartridge 22. it can.

【0018】[0018]

【発明の効果】以上のように本発明によれば、膜カート
リッジの製造時に付与する力によって、使用時にろ過膜
を常に緊張状態に維持するので、上昇流によって上方へ
付勢力を受けても、ろ過膜は煽られることがなく、常に
平坦な膜面を維持することができ、止水部Sで疲労破壊
が起こることがなく、膜カートリッジの寿命を延ばすこ
とができ、常に平坦な膜面を維持することで、上昇流が
膜面の全体に均一に掃流として作用し、洗浄効果が高ま
る。
As described above, according to the present invention, the filter membrane is always kept in tension during use by the force applied during the manufacture of the membrane cartridge. The filtration membrane is not lifted, can always maintain a flat membrane surface, does not cause fatigue destruction in the water stop portion S, can extend the life of the membrane cartridge, and can always maintain a flat membrane surface. By maintaining it, the upward flow uniformly acts as a scavenging flow on the entire film surface, and the cleaning effect is enhanced.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の実施の形態における膜カートリッジの
製造方法を示す模式図である。
FIG. 1 is a schematic view illustrating a method for manufacturing a membrane cartridge according to an embodiment of the present invention.

【図2】同実施の形態において製造した膜カートリッジ
を示す模式図である。
FIG. 2 is a schematic view showing a membrane cartridge manufactured in the same embodiment.

【図3】本発明の実施の形態における膜カートリッジの
製造方法を示す模式図である。
FIG. 3 is a schematic view illustrating a method for manufacturing a membrane cartridge according to an embodiment of the present invention.

【図4】同実施の形態において製造した膜カートリッジ
を示す模式図である。
FIG. 4 is a schematic view showing a membrane cartridge manufactured in the same embodiment.

【図5】浸漬型膜分離装置を示す模式図である。FIG. 5 is a schematic view showing an immersion type membrane separation device.

【図6】従来の膜カートリッジを示す正面図である。FIG. 6 is a front view showing a conventional membrane cartridge.

【図7】従来の膜カートリッジの使用状態を示す模式図
である。
FIG. 7 is a schematic view showing a state of use of a conventional membrane cartridge.

【符号の説明】[Explanation of symbols]

21 膜分離装置 22 膜カートリッジ 22A ろ板 22B ろ過膜 23 散気装置 21 membrane separator 22 membrane cartridge 22A filter plate 22B filtration membrane 23 air diffuser

フロントページの続き (72)発明者 上島 達也 大阪府大阪市浪速区敷津東一丁目2番47号 株式会社クボタ内 (72)発明者 永野 昌章 大阪府大阪市浪速区敷津東一丁目2番47号 株式会社クボタ内 (72)発明者 岡島 康信 大阪府大阪市浪速区敷津東一丁目2番47号 株式会社クボタ内 (72)発明者 藤原 幸男 大阪府大阪市浪速区敷津東一丁目2番47号 株式会社クボタ内 Fターム(参考) 4D006 GA02 HA41 HA91 HA93 JA07B JA07C JA22Z JB04 JB07 KA31 KA44 KB22 KC03 KC16 KD16 KD24 MA03 MA06 MA31 MA40 MC48X PA01 PB08 PC62 PC65 4D028 AB00 BC17 Continued on the front page (72) Inventor Tatsuya Uejima 2-47, Shikitsu-Higashi 1-chome, Namiwa-ku, Osaka-shi, Osaka (72) Inventor Masaaki Nagano 1-2-1-2, Shikitsu-higashi, Naniwa-ku, Osaka, Osaka No. 47 Kubota Co., Ltd. (72) Inventor Yasunobu Okajima 2-47 Shikitsu Higashi 1-chome, Naniwa-ku, Osaka-shi, Osaka No. 47 Inventor Yukio Fujiwara Yukio Fujiwara 1-chome, Shikitsu-Higashi, Naniwa-ku, Osaka, Osaka No. 47 No. 47 F-term in Kubota Corporation (Reference) 4D006 GA02 HA41 HA91 HA93 JA07B JA07C JA22Z JB04 JB07 KA31 KA44 KB22 KC03 KC16 KD16 KD24 MA03 MA06 MA31 MA40 MC48X PA01 PB08 PC62 PC65 4D028 AB00 BC17

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 樹脂製のろ板を所定冷却温度下で冷却
し、冷却により収縮した状態のろ板に表面を覆ってろ過
膜を配置し、ろ板の周縁部に沿った全周にわたって形成
する止水部においてろ過膜をろ板に接着もしくは溶着し
て固定し、ろ板が使用温度下において伸長することによ
りろ過膜に引張力を付与して緊張させることを特徴とす
る浸漬型膜カートリッジの製造方法。
1. A filter plate made of resin is cooled at a predetermined cooling temperature, and a filter membrane is arranged so as to cover the surface of the filter plate that has been contracted by cooling, and formed over the entire periphery along the periphery of the filter plate. A immersion type membrane cartridge characterized in that a filtration membrane is adhered or welded to a filter plate at a water stop portion to be fixed, and the filter plate is stretched at an operating temperature to apply a tensile force to the filtration membrane to tension it. Manufacturing method.
【請求項2】 樹脂製のろ板に表面を覆ってろ過膜を緊
張状態に配置し、ろ板の周縁部に沿った全周にわたって
形成する止水部においてろ過膜をろ板に接着もしくは溶
着して固定し、ろ過膜を緊張状態に保持することを特徴
とする浸漬型膜カートリッジの製造方法。
2. A filter membrane is placed in tension on a resin filter plate so as to cover the surface thereof, and the filter membrane is adhered or welded to the filter plate at a water stop portion formed over the entire periphery along the peripheral edge of the filter plate. A method for producing a submerged membrane cartridge, comprising fixing the filtration membrane in a tensioned state.
【請求項3】 樹脂製のろ板を所定冷却温度下で冷却
し、冷却により収縮した状態のろ板に表面を覆ってろ過
膜を緊張状態に配置し、ろ板の周縁部に沿った全周にわ
たって形成する止水部においてろ過膜をろ板に接着もし
くは溶着して固定し、ろ板が使用温度下において伸長す
ることによりろ過膜に引張力を付与して緊張させること
を特徴とする浸漬型膜カートリッジの製造方法。
3. A filter plate made of resin is cooled at a predetermined cooling temperature, and a filter membrane is placed in a tensioned state so as to cover the surface of the filter plate contracted by cooling so as to cover the surface thereof. An immersion characterized in that the filter membrane is adhered or welded to the filter plate at the water stop portion formed over the periphery and fixed thereto, and the filter plate is stretched at the operating temperature to apply a tensile force to the filter membrane to cause tension. Manufacturing method of mold membrane cartridge.
JP29172799A 1999-10-14 1999-10-14 Production method of immersion type membrane cartridge Pending JP2001113138A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29172799A JP2001113138A (en) 1999-10-14 1999-10-14 Production method of immersion type membrane cartridge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29172799A JP2001113138A (en) 1999-10-14 1999-10-14 Production method of immersion type membrane cartridge

Publications (1)

Publication Number Publication Date
JP2001113138A true JP2001113138A (en) 2001-04-24

Family

ID=17772626

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29172799A Pending JP2001113138A (en) 1999-10-14 1999-10-14 Production method of immersion type membrane cartridge

Country Status (1)

Country Link
JP (1) JP2001113138A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7776214B2 (en) 2005-02-23 2010-08-17 Gs Yuasa Corporation Membrane element

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7776214B2 (en) 2005-02-23 2010-08-17 Gs Yuasa Corporation Membrane element

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